Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems
Autor(a) principal: | |
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Data de Publicação: | 2017 |
Outros Autores: | , , , , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Repositório Institucional da UNESP |
Texto Completo: | http://dx.doi.org/10.1016/j.fluid.2017.07.005 http://hdl.handle.net/11449/169959 |
Resumo: | Clavulanic acid (CA) is an important pharmaceutical compound produced by batch fermentation of Streptomyces clavuligerus. Since, CA is chemically unstable, its downstream processing should be studied to develop more efficient and resolute techniques. Herein, the use of aqueous two-phase systems (ATPS) composed of cholinium chloride, [Ch]Cl, was proposed as a novel platform for the recovery and purification of CA. Thus, the stability of CA in presence of different [Ch]Cl concentrations was initially studied, and the high biocompatibility of this salt was demonstrated by the low CA degradation levels. Then, the partitioning of CA using two types of polymeric ATPS has been investigated. Two ATPS formed by the combination of [Ch]Cl and two polyethylene glycol (PEG) polymers, PEG 600 g mol−1 (PEG-600) and polyethylene glycol methyl ether 550 g mol−1 (PEG-500-OMe), were used to assess the influence of the PEG nature, in addition to the concentration of the phase forming agents on the CA partitioning. It has shown that CA is almost equally distributed between the two-phases in equilibrium (0.6 < KCA < 1.6). Nevertheless, the selective extraction of CA for the [Ch]Cl-rich or PEG-rich phase by the proper adjustment of ATPS composition was attained. In the search for higher extraction efficiencies [EE (%)] and partition coefficients (KCA), a second polymeric ATPS platform composed of PEG-600 and sodium polyacrylate 8000 g mol−1 (NaPA-8000), applying [Ch]Cl as adjuvant was tested. The main results suggest the recovery of CA towards the PEG-rich phase (KCA ≥ 5.6 ± 0.6 and EE ≥ 85.5± 1.4%). The higher migration levels of CA have mainly resulted from the electronegative repulsion of NaPA-8000 over CA molecules. The ATPS with best performance for the CA extraction were selected for the recovery of CA directly from fermented broth of Streptomyces clavuligerus. In this set of experiments, the highest values of CA recovery yield and purification factor (respectively, 64.91± 1.99% and 22.70 ± 0.87) were attained for the systems PEG-600/NaPA-8000 and PEG-600/[Ch]Cl, respectively. |
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Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systemsAqueous two-phase systemsCholinium chlorideClavulanic acidPolyethylene glycolStreptomyces clavuligerusClavulanic acid (CA) is an important pharmaceutical compound produced by batch fermentation of Streptomyces clavuligerus. Since, CA is chemically unstable, its downstream processing should be studied to develop more efficient and resolute techniques. Herein, the use of aqueous two-phase systems (ATPS) composed of cholinium chloride, [Ch]Cl, was proposed as a novel platform for the recovery and purification of CA. Thus, the stability of CA in presence of different [Ch]Cl concentrations was initially studied, and the high biocompatibility of this salt was demonstrated by the low CA degradation levels. Then, the partitioning of CA using two types of polymeric ATPS has been investigated. Two ATPS formed by the combination of [Ch]Cl and two polyethylene glycol (PEG) polymers, PEG 600 g mol−1 (PEG-600) and polyethylene glycol methyl ether 550 g mol−1 (PEG-500-OMe), were used to assess the influence of the PEG nature, in addition to the concentration of the phase forming agents on the CA partitioning. It has shown that CA is almost equally distributed between the two-phases in equilibrium (0.6 < KCA < 1.6). Nevertheless, the selective extraction of CA for the [Ch]Cl-rich or PEG-rich phase by the proper adjustment of ATPS composition was attained. In the search for higher extraction efficiencies [EE (%)] and partition coefficients (KCA), a second polymeric ATPS platform composed of PEG-600 and sodium polyacrylate 8000 g mol−1 (NaPA-8000), applying [Ch]Cl as adjuvant was tested. The main results suggest the recovery of CA towards the PEG-rich phase (KCA ≥ 5.6 ± 0.6 and EE ≥ 85.5± 1.4%). The higher migration levels of CA have mainly resulted from the electronegative repulsion of NaPA-8000 over CA molecules. The ATPS with best performance for the CA extraction were selected for the recovery of CA directly from fermented broth of Streptomyces clavuligerus. In this set of experiments, the highest values of CA recovery yield and purification factor (respectively, 64.91± 1.99% and 22.70 ± 0.87) were attained for the systems PEG-600/NaPA-8000 and PEG-600/[Ch]Cl, respectively.Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Federación Española de Enfermedades RarasDepartment of Bioprocess and Biotechnology School of Pharmaceutical Sciences UNESP – Univ Estadual Paulista, Rodovia Araraquara-Jaú/01, Campos VilleInstitute of Botany Leibniz Universität Hannover, Herrenhäuser Str. 2CICECO – Aveiro Institute of Materials Department of Chemistry University of AveiroDepartment of Bioprocess and Biotechnology School of Pharmaceutical Sciences UNESP – Univ Estadual Paulista, Rodovia Araraquara-Jaú/01, Campos VilleFAPESP: 2014/01580-3Federación Española de Enfermedades Raras: PT2020Universidade Estadual Paulista (Unesp)Leibniz Universität HannoverUniversity of AveiroPanas, Paweł [UNESP]Lopes, Camila [UNESP]Cerri, Marcel O. [UNESP]Ventura, Sónia P.M.Santos-Ebinuma, Valéria C. [UNESP]Pereira, Jorge F.B. [UNESP]2018-12-11T16:48:26Z2018-12-11T16:48:26Z2017-10-25info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article42-50application/pdfhttp://dx.doi.org/10.1016/j.fluid.2017.07.005Fluid Phase Equilibria, v. 450, p. 42-50.0378-3812http://hdl.handle.net/11449/16995910.1016/j.fluid.2017.07.0052-s2.0-850256287782-s2.0-85025628778.pdfScopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengFluid Phase Equilibria0,950info:eu-repo/semantics/openAccess2024-01-03T06:21:15Zoai:repositorio.unesp.br:11449/169959Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T22:00:08.131065Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false |
dc.title.none.fl_str_mv |
Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems |
title |
Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems |
spellingShingle |
Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems Panas, Paweł [UNESP] Aqueous two-phase systems Cholinium chloride Clavulanic acid Polyethylene glycol Streptomyces clavuligerus |
title_short |
Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems |
title_full |
Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems |
title_fullStr |
Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems |
title_full_unstemmed |
Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems |
title_sort |
Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems |
author |
Panas, Paweł [UNESP] |
author_facet |
Panas, Paweł [UNESP] Lopes, Camila [UNESP] Cerri, Marcel O. [UNESP] Ventura, Sónia P.M. Santos-Ebinuma, Valéria C. [UNESP] Pereira, Jorge F.B. [UNESP] |
author_role |
author |
author2 |
Lopes, Camila [UNESP] Cerri, Marcel O. [UNESP] Ventura, Sónia P.M. Santos-Ebinuma, Valéria C. [UNESP] Pereira, Jorge F.B. [UNESP] |
author2_role |
author author author author author |
dc.contributor.none.fl_str_mv |
Universidade Estadual Paulista (Unesp) Leibniz Universität Hannover University of Aveiro |
dc.contributor.author.fl_str_mv |
Panas, Paweł [UNESP] Lopes, Camila [UNESP] Cerri, Marcel O. [UNESP] Ventura, Sónia P.M. Santos-Ebinuma, Valéria C. [UNESP] Pereira, Jorge F.B. [UNESP] |
dc.subject.por.fl_str_mv |
Aqueous two-phase systems Cholinium chloride Clavulanic acid Polyethylene glycol Streptomyces clavuligerus |
topic |
Aqueous two-phase systems Cholinium chloride Clavulanic acid Polyethylene glycol Streptomyces clavuligerus |
description |
Clavulanic acid (CA) is an important pharmaceutical compound produced by batch fermentation of Streptomyces clavuligerus. Since, CA is chemically unstable, its downstream processing should be studied to develop more efficient and resolute techniques. Herein, the use of aqueous two-phase systems (ATPS) composed of cholinium chloride, [Ch]Cl, was proposed as a novel platform for the recovery and purification of CA. Thus, the stability of CA in presence of different [Ch]Cl concentrations was initially studied, and the high biocompatibility of this salt was demonstrated by the low CA degradation levels. Then, the partitioning of CA using two types of polymeric ATPS has been investigated. Two ATPS formed by the combination of [Ch]Cl and two polyethylene glycol (PEG) polymers, PEG 600 g mol−1 (PEG-600) and polyethylene glycol methyl ether 550 g mol−1 (PEG-500-OMe), were used to assess the influence of the PEG nature, in addition to the concentration of the phase forming agents on the CA partitioning. It has shown that CA is almost equally distributed between the two-phases in equilibrium (0.6 < KCA < 1.6). Nevertheless, the selective extraction of CA for the [Ch]Cl-rich or PEG-rich phase by the proper adjustment of ATPS composition was attained. In the search for higher extraction efficiencies [EE (%)] and partition coefficients (KCA), a second polymeric ATPS platform composed of PEG-600 and sodium polyacrylate 8000 g mol−1 (NaPA-8000), applying [Ch]Cl as adjuvant was tested. The main results suggest the recovery of CA towards the PEG-rich phase (KCA ≥ 5.6 ± 0.6 and EE ≥ 85.5± 1.4%). The higher migration levels of CA have mainly resulted from the electronegative repulsion of NaPA-8000 over CA molecules. The ATPS with best performance for the CA extraction were selected for the recovery of CA directly from fermented broth of Streptomyces clavuligerus. In this set of experiments, the highest values of CA recovery yield and purification factor (respectively, 64.91± 1.99% and 22.70 ± 0.87) were attained for the systems PEG-600/NaPA-8000 and PEG-600/[Ch]Cl, respectively. |
publishDate |
2017 |
dc.date.none.fl_str_mv |
2017-10-25 2018-12-11T16:48:26Z 2018-12-11T16:48:26Z |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://dx.doi.org/10.1016/j.fluid.2017.07.005 Fluid Phase Equilibria, v. 450, p. 42-50. 0378-3812 http://hdl.handle.net/11449/169959 10.1016/j.fluid.2017.07.005 2-s2.0-85025628778 2-s2.0-85025628778.pdf |
url |
http://dx.doi.org/10.1016/j.fluid.2017.07.005 http://hdl.handle.net/11449/169959 |
identifier_str_mv |
Fluid Phase Equilibria, v. 450, p. 42-50. 0378-3812 10.1016/j.fluid.2017.07.005 2-s2.0-85025628778 2-s2.0-85025628778.pdf |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
Fluid Phase Equilibria 0,950 |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
42-50 application/pdf |
dc.source.none.fl_str_mv |
Scopus reponame:Repositório Institucional da UNESP instname:Universidade Estadual Paulista (UNESP) instacron:UNESP |
instname_str |
Universidade Estadual Paulista (UNESP) |
instacron_str |
UNESP |
institution |
UNESP |
reponame_str |
Repositório Institucional da UNESP |
collection |
Repositório Institucional da UNESP |
repository.name.fl_str_mv |
Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP) |
repository.mail.fl_str_mv |
|
_version_ |
1808129382579961856 |